PHYSICOCHEMICAL ASPECTS OF FLUID EXTRACTION

[1] VOLUMETRIC AND PHASE BEHAVIOR OF NITROGEN-HYDROCARBON SYSTEMS - NITROGEN-BUTANE SYSTEM [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12): : 2539 - 2540

[2] FLUID MIXTURES AT HIGH-PRESSURE - PHASE SEPARATION AND CRITICAL PHENOMENA IN BINARY-MIXTURES OF A POLAR COMPONENT WITH SUPERCRITICAL CARBON-DIOXIDE, ETHANE, AND ETHENE UP TO 1000 BAR [J]. BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1976, 80 (12): : 1310 - 1315

[3] OPTOELECTRICAL METHOD FOR MEASUREMENT OF PRESSURE AND FOR INVESTIGATION OF PHASE-EQUILIBRIUM OF DEEPLY COLORED OR TURBID MIXTURES UNDER HIGH-PRESSURES [J]. REVIEW OF SCIENTIFIC INSTRUMENTS, 1978, 49 (07) : 944 - 947

[4] Angus S., 1976, INT THERMODYNAMIC TA

[5] THE STATE OF THE ART OF EXTRACTION WITH COMPRESSED GASES [J]. CHEMIE INGENIEUR TECHNIK, 1981, 53 (07) : 529 - 542

[6] VAPORISATION EQUILIBRIA AND CRITICAL CURVES FOR SYSTEMS ETHANE/WATER AND N-BUTANE/WATER AT HIGH PRESSURES [J]. CHEMIE INGENIEUR TECHNIK, 1967, 39 (13) : 816 - &

[7] A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .2. APPLICATION TO PURE SUBSTANCES [J]. CHEMICAL ENGINEERING SCIENCE, 1981, 36 (07) : 1147 - 1151

[8] A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .1. DERIVATION [J]. CHEMICAL ENGINEERING SCIENCE, 1981, 36 (07) : 1139 - 1146

[9] FLUID MIXTURES AT HIGH-PRESSURES - COMPUTER CALCULATIONS OF PHASE-EQUILIBRIA AND CRITICAL PHENOMENA IN FLUID BINARY-MIXTURES FROM REDLICH-KWONG EQUATION OF STATE [J]. BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1976, 80 (12): : 1316 - 1321

[10] A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .3. APPLICATION TO PHASE-EQUILIBRIA IN BINARY-MIXTURES [J]. CHEMICAL ENGINEERING SCIENCE, 1982, 37 (06) : 855 - 861

[1] VOLUMETRIC AND PHASE BEHAVIOR OF NITROGEN-HYDROCARBON SYSTEMS - NITROGEN-BUTANE SYSTEM [J]. INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12): : 2539 - 2540

[2] FLUID MIXTURES AT HIGH-PRESSURE - PHASE SEPARATION AND CRITICAL PHENOMENA IN BINARY-MIXTURES OF A POLAR COMPONENT WITH SUPERCRITICAL CARBON-DIOXIDE, ETHANE, AND ETHENE UP TO 1000 BAR [J]. BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1976, 80 (12): : 1310 - 1315

[3] OPTOELECTRICAL METHOD FOR MEASUREMENT OF PRESSURE AND FOR INVESTIGATION OF PHASE-EQUILIBRIUM OF DEEPLY COLORED OR TURBID MIXTURES UNDER HIGH-PRESSURES [J]. REVIEW OF SCIENTIFIC INSTRUMENTS, 1978, 49 (07) : 944 - 947

[4] Angus S., 1976, INT THERMODYNAMIC TA

[5] THE STATE OF THE ART OF EXTRACTION WITH COMPRESSED GASES [J]. CHEMIE INGENIEUR TECHNIK, 1981, 53 (07) : 529 - 542

[6] VAPORISATION EQUILIBRIA AND CRITICAL CURVES FOR SYSTEMS ETHANE/WATER AND N-BUTANE/WATER AT HIGH PRESSURES [J]. CHEMIE INGENIEUR TECHNIK, 1967, 39 (13) : 816 - &

[7] A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .2. APPLICATION TO PURE SUBSTANCES [J]. CHEMICAL ENGINEERING SCIENCE, 1981, 36 (07) : 1147 - 1151

[8] A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .1. DERIVATION [J]. CHEMICAL ENGINEERING SCIENCE, 1981, 36 (07) : 1139 - 1146

[9] FLUID MIXTURES AT HIGH-PRESSURES - COMPUTER CALCULATIONS OF PHASE-EQUILIBRIA AND CRITICAL PHENOMENA IN FLUID BINARY-MIXTURES FROM REDLICH-KWONG EQUATION OF STATE [J]. BERICHTE DER BUNSEN-GESELLSCHAFT-PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 1976, 80 (12): : 1316 - 1321

[10] A NEW SEMI-EMPIRICAL EQUATION OF STATE FOR FLUIDS .3. APPLICATION TO PHASE-EQUILIBRIA IN BINARY-MIXTURES [J]. CHEMICAL ENGINEERING SCIENCE, 1982, 37 (06) : 855 - 861